石油炼制与化工 ›› 2012, Vol. 43 ›› Issue (11): 27-30.

• 催化剂 • 上一篇    下一篇

Prime-G+技术在催化裂化汽油加氢脱硫装置上的应用

董海明1,曲云2,孙丽琳1   

  1. 1. 中国石油兰州石化公司炼油厂   2. 中国石油兰州石化公司研究院
  • 收稿日期:2012-02-28 修回日期:2012-05-16 出版日期:2012-11-12 发布日期:2012-10-31
  • 通讯作者: 曲云 E-mail:quyun@petrochina.com.cn

APPLICATION OF PRIME-G+ TECHNOLOGY IN FCC NAPHTHA HYDRODESULFURIZATION UNIT

  • Received:2012-02-28 Revised:2012-05-16 Online:2012-11-12 Published:2012-10-31

摘要: 为使出厂汽油硫含量达到国Ⅳ汽油排放标准,中国石油兰州石化公司引进法国Prime-G+技术建成1套1.8 Mt/a催化裂化汽油加氢脱硫装置。标定结果表明:装置加工硫质量分数为195 μg/g的催化裂化汽油时,所得混合汽油产品硫质量分数为38.5 μg/g,硫醇硫质量分数为3.5 μg/g;研究法辛烷值损失为1个单位,达到设计(不大于1.8个单位)的要求;混合汽油产品的收率为99.91%,高于设计值(99.90%);能耗为934.6 MJ/t,低于设计值(937.2 MJ/t)。在满负荷条件下装置运行较为平稳,经济效益明显,每年可增加效益6.9亿元。

Abstract: To meet the sulfur content of gasoline product satisfying national emission standard Ⅳ, a 1.8 Mt/a hydrodesulfurization unit processing FCC naphtha feed was built at Lanzhou Petrochemical Company adopting Prime-G+ technology. Performance test data of this unit show that when processing FCC naphtha with sulfur content of 195 μg/g, the obtained mixed gasoline product has total sulfur content and mercaptaneous sulfur content of 38.5 μg/g and 3.5 μg/g, respectively. The RON loss of the gasoline product is 1 unit, which is less than the design value (1.8 units). Furthermore, the yield of mixed gasoline product was 99.91% which is a bit higher than the design value (99.90%), and the energy consumption was 934.6 MJ/t which is lower than the design value (937.2 MJ/t). The unit is operated stably under full-capacity with significant economic efficiency, an increment of 690 MRMB annually.